scholarly journals Reliability and efficiency of an advanced tertiary treatment process for wastewater reclamation

2019 ◽  
Vol 9 (4) ◽  
pp. 385-395 ◽  
Author(s):  
Hongbin Xu ◽  
Jaap de Koning ◽  
Ying Geng

Abstract A reliability study for the reclamation of wastewater treatment plant effluent using continuous sand filtration-multimedia filtration (CSF-MMF) combined with ultrafiltration (UF) and reverse osmosis (RO) has been conducted. The objectives of the research are two-fold: (1) effluent of CSF-MMF can be used for surface water supplementation and (2) permeate of UF-RO can be applied as greenhouse irrigation water. The removal efficiencies for nutrients and electric conductivity (EC) as well as some operational parameters of the pilot plant were investigated. The concentration of T-N, chemical oxygen demand (COD) and turbidity in the filtrate of CSF-MMF with external C-course methanol dosage and FeCl3 dosage could be kept at less than 2.2 mg/L, 35 mg/L and 0.9 NTU respectively. Average EC exceeded the required surface water standard by 10% and it was difficult to meet the low surface water standard for T-P (below 0.15 mg/L). The EC of RO permeate was below 20 μS/cm, which was much lower than the standard for greenhouse irrigation. With frequent back flushes, cleaning in place (CIP) and enhanced cleaning the UF could be operated with a constant permeability of 100 L/(m2·h·bar). An appropriate CIP resulted in a recovery of 47–52% of the RO. The protective cartridge filter prior to the RO should be replaced every 2 weeks.

1995 ◽  
Vol 31 (12) ◽  
pp. 399-408 ◽  
Author(s):  
R. M. Fuog ◽  
K. C. Giberson ◽  
R. L. Lawrence

Rancho Murieta is an exclusive 1,400 ha (3,500 acre) master-planned golf-course-oriented community and is located approximately 39 km (24 miles) southeast of Sacramento, the capital of California. The community located along the banks of the Cosumnes River, one of the last pristine rivers in California, is situated in the great Central Valley of California which enjoys a Mediterranean-like semi-arid climate. The community has a present population of 3,500 people and is projected to have an ultimate population of 15,600. The Rancho Murieta Community Services District provides wastewater collection treatment and disposal services, among others within the community. In the early 1980s, the District obtained 55 ha (135 acres) of land for a wastewater treatment facility from the original developer of the community. Despite the immediate proximity of the plant to the Cosumnes River, the District was not allowed to discharge any plant effluent to the river. In favor of preserving the pristine qualities of the river, a “zero discharge” was required. Therefore, the District had to provide for some form of reuse of its effluent, a land disposal alternative. After considerable study, a plan was developed to integrate the community's two proposed championship golf courses into a comprehensive wastewater reclamation program. In addition to significantly decreasing the demand for treated domestic water within the community, a comprehensive program to irrigate the golf courses with reclaimed wastewater would also significantly lower the summertime demand for water from the river, thereby providing increased flows to downstream agricultural users along the river, a true “win-win” situation for all parties concerned. In order to provide treatment to an acceptable level for irrigation of golf courses surrounded by dwellings, it was decided that a tertiary treatment plant would be designed to meet California's wastewater reclamation requirements. The current treatment plant was constructed in three phases. California has very strict standards for effluent reuse and they are described in Title 22 of the California Code of Regulations. Use of reclaimed wastewater for most golf courses requires oxidation, coagulation, filtration and disinfection. The effluent has to meet a 2 NTU turbidity and 2.2 MPN/100 coliform standard. To comply with these standards, the District developed a unique treatment process that has allowed the District to be in full compliance since start-up without a single violation of the plant's discharge requirements. The initial treatment process consists of oxidation ponds. Mechanical aerators are located on the ponds to ensure that sufficient oxygen is provided at all times for treatment and most importantly for odor control. The pond effluent is discharged into two large reservoirs. These two reservoirs are sized to store wastewater for up to 150 days during periods of non-irrigation. When irrigation can be performed on the golf course, the tertiary treatment process is activated. It consists of dissolved air flotation for algae removal, filtration for polishing, and disinfection. Treatment design parameters, effluent quality results and capital and operating costs are presented.


2006 ◽  
Vol 54 (3) ◽  
pp. 23-28 ◽  
Author(s):  
J. Rapala ◽  
M. Niemelä ◽  
K.A. Berg ◽  
L. Lepistö ◽  
K. Lahti

The removal of cyanobacteria, hepatotoxins produced by them (microcystins), phytoplankton, heterotrophic bacteria and endotoxins were monitored at a surface water treatment plant with coagulation, clarification, sand filtration, ozonation, slow sand filtration and chlorination as the treatment process. Coagulation–sand filtration reduced microcystins by 1.2–2.4, and endotoxins by 0.72–2.0 log10 units. Ozonation effectively removed the residual microcystins. The treatment process reduced phytoplankton biomass by 2.2–4.6 and heterotrophic bacteria by 2.0–5.0 log10 units. In treated water, the concentration of microcystins never exceeded the WHO guide value (1 μg/L), but picoplankton and monad cells were often detected in high numbers. The heterotrophic bacterial isolates from the treated waters belonged to genera Sphingomonas, Pseudomonas, Bacillus, Herbaspirillum and Bosea.


2015 ◽  
Vol 6 (1) ◽  
pp. 72-81 ◽  
Author(s):  
Joaquín Melgarejo ◽  
Daniel Prats ◽  
Andrés Molina ◽  
Arturo Trapote

In Spain, and particularly in the Valencia Region, the scarcity of water resources means that water resource exploitation must be optimized. In this light, reusing the large amounts of treated wastewater is a top priority, especially in agriculture, urban use and the irrigation of golf courses. Rincón de León wastewater treatment plant–water reclamation plant (Alicante, Spain) supplies reclaimed flow to a number of users according to the guidelines stated in the Royal Decree 1620/2007. Reclamation treatment includes: coagulation + flocculation + filtration (sand bed), ultrafiltration, ultraviolet disinfection and desalination (reverse osmosis). By combining these processes, three tertiary treatment alternatives were configured, and for each of them the quality of effluents, treatment costs, energy consumption and the uses of treated water were analysed. The results show that the quality of the water treated using the three alternatives is suitable for different uses. Moreover, the costs resulting from the tertiary treatment processes, their energy consumption and the final price of the treated water paid by farmers have been obtained.


Author(s):  
João Antônio Monteiro Florênço ◽  
Lucas Zanon Scherolt ◽  
Viviane Trevisan ◽  
Everton Skoronski

The objective of this study was to evaluate the efficiency of the wetlands cultivated with sunflower and soybean in the removal of Chemical Oxygen Demand, ammonia, nitrate, nitrite, total phosphorus and Kjeldahl Total Nitrogen (KTN) of the treated leachate from the landfill treatment plant of the city of Lages / SC. It was also analyzed the plants development as a function of the effluent applied in the wetlands compared to wetlands irrigated with chemical fertilizer. The wetlands were operated in batch with hydraulic retention times (HRT) of 2 and 4 days, receiving treated slurry in concentrations of 10 and 25% and liquid chemical fertilizer (5 ml / L). In the tests carried out with HRT of 4 days only the concentrations of COD and of ammonia were analyzed. After 4 months, the plants size was measured to verify their growth. In the tests carried out with the soybean there was no germination of the seeds. In both HRT tested, a greater removal of phosphorus, ammonia, nitrite and KTN was observed when 25% concentration of leachate. It was observed that the sunflower plants showed a higher size when cultivated in wetlands operated with HRT of 4 days and that they received the treated leachate in the concentration of 10%.


2009 ◽  
Vol 1 (1) ◽  
pp. 8-12
Author(s):  
V. K. Tyagi ◽  
A. K. Chopra ◽  
N. C. Durgapal ◽  
A. A. Kazmi

This paper investigates the utility and validity of bioassay toxicity testing using Daphnia magna straus as test organism for monitoring the common effluent treatment plant (CETP) receiving both industrial as well as domestic effluent. The average daphnia toxicity (Gd) at inlet, after primary settling tank (PST), secondary settling tank (SST) and tertiary treatment unit were reported as Gd-16, Gd-12, Gd-4 and Gd-1 respectively. However, a cumulative percentage removal in toxicity after PST, SST and tertiary treatment units was observed as 25%, 75% and 100%, respectively, during entire study period. It showed that a complete removal in daphnia toxicity (Gd) i.e.100% had been achieved only after tertiary treatment unit involving Dual Media Filters followed by activated carbon filters. Further attempts have been made to establish the relationship between key wastewater constituents i.e. Chemical Oxygen Demand (COD) and Suspended Solids (SS) with respects to daphnia toxicity (Gd). It was observed that COD and SS show a statistically significant correlation (r2) with daphnia toxicity (Gd) i.e. 0.89 and 0.81, respectively. Thus COD and SS can serve as a regulatory tool in lieu of an explicit toxicity standard (to check and improve the operational status of wastewatertreatment plants in time).


2013 ◽  
Vol 68 (9) ◽  
pp. 2012-2018 ◽  
Author(s):  
Wioleta Kocerba-Soroka ◽  
Edyta Fiałkowska ◽  
Agnieszka Pajdak-Stós ◽  
Mateusz Sobczyk ◽  
Małgorzata Pławecka ◽  
...  

The influence of a high density of rotifers, which is known to be able to control filamentous bacteria, on the parameters of an activated sludge process was examined in four professional laboratory batch reactors. These reactors allow the imitation of the work of a wastewater treatment plant with enhanced nutrient removal. The parameters, including oxygen concentration, pH and temperature, were constantly controlled. The experiment showed that Lecane rotifers are able to proliferate in cyclically anaerobic/anoxic and aerobic conditions and at dissolved oxygen concentrations as low as 1 mg/L. In 1 week, rotifer density increased fivefold, exceeding the value of 2,200 ind./mL. The grazing activity led to an improvement in settling properties. Extremely high numbers of rotifers did not affect the main parameters, chemical oxygen demand (COD), N-NH4, N-NO3, P-PO4 and pH, during sewage treatment. Therefore, the use of rotifers as a tool to limit the growth of filamentous bacteria appears to be safe for the entire wastewater treatment process.


2008 ◽  
Vol 57 (8) ◽  
pp. 1235-1240 ◽  
Author(s):  
James L. Barnard ◽  
Thomas E. Kunetz ◽  
Joseph P. Sobanski

The Stickney plant of the Metropolitan Wastewater Reclamation District of Greater Chicago (MWRDGC), one of the largest wastewater treatment plants in the world, treats an average dry weather flow of 22 m3/s and a sustained wet weather flow of 52 m3/s that can peak to 63 m3/s. Most of the inner city of Chicago has combined sewers, and in order to reduce pollution through combined sewer overflows (CSO), the 175 km Tunnel and Reservoir Plan (TARP) tunnels, up to 9.1 m in diameter, were constructed to receive and convey CSO to a reservoir from where it will be pumped to the Stickney treatment plant. Pumping back storm flows will result in sustained wet weather flows over periods of weeks. Much of the success of the plant will depend on the ability of 96 circular final clarifiers to produce an effluent of acceptable quality. The nitrifying activated sludge plant is arranged in a plug-flow configuration, and some denitrification takes place as a result of the high oxygen demand in the first pass of the four-pass aeration basins that have a length to width ratio of 18:1. The SVI of the mixed liquor varies between 60 and 80 ml/g. The final clarifiers, which were designed by the District's design office in 1938, have functioned for more than 65 years without major changes and are still producing very high-quality effluent. This paper will discuss the design and operation of these final clarifiers and compare the design with more modern design practices.


2018 ◽  
Vol 6 (7) ◽  
pp. 278-289
Author(s):  
Serajuddin ◽  
Aktarul Islam Chowdhury ◽  
Tahmina Ferdous

Organic matter in drinking water is determined by applying indirect determination methods used for quantitative measurements such as total organic carbon (TOC), chemical oxygen demand (COD), and biochemical oxygen demand (BOD). As a relatively less sophisticated and faster method ultraviolet absorption of water at 254 nm wavelength (UV254) is being now utilized in many countries to determine the organic matter in water. Because the UV254 absorbance parameter is proportional to the concentration of organics in the water in many research it is found that most natural water sources have a good correlation between, for example, TOC and UV254 absorption, and COD and UV254 absorption. Similarly, a definite correlation between the COD and BOD under certain conditions was reported in the literature. This study is aimed to establish the correlations among the parameters namely UV254, COD, BOD5, TOC, DOC (Dissolve organic carbon) for the river Sitalakhya, a specific surface water, which is the raw water source of the largest surface water treatment plant in Dhaka, Bangladesh. It is revealed that there is a very strong correlation between TOC and UV254 with R2=0.86. Similarly, between BOD5 and UV254, and between COD and UV254, a strong correlation was found with coefficient of determination, R2 value respectively 0.93 and 0.87. All other coefficients also indicate highly significant linear correlations.


2004 ◽  
Vol 48 (11-12) ◽  
pp. 337-344 ◽  
Author(s):  
P. Battistoni ◽  
R. Boccadoro ◽  
D. Bolzonella ◽  
M. Marinelli

A simple mathematical model of an alternate oxic-anoxic process has been elaborated. It enables us to optimise the cycle time on the basis of maximum nitrates concentration in the effluent and the desired nitrogen removal performance. At the same time the model can be employed to verify the impact of the variations of flow rate and influent characteristics as well as the operational parameters of the process. Actually, the model confirms the process efficiency but its feasibility in real plants needs a local or remote process control. To verify these theoretical conclusions a real wastewater plant (700 PE) has been upgraded in an alternate oxic-anoxic process. It was implemented with software able to elaborate the data of dissolved oxygen concentration and oxidation reduction potential. Moreover, the evaluation of the flexing points was performed to manage mixer and blowers. A one-year experience of plant management allowed us to obtain very high nitrogen removal. However, the performances were different during wet or dry weather periods. The statistical analysis of probe signals evaluation confirmed the capability of the control device to detect the flexing points during the anoxic phase (70-94%). On the other hand, the capability of detecting the DO signal was lower, in particular when the oxygen demand was similar to the amount of supplied oxygen. The hourly variations of flow rate and mass loading determines different conditions for starting the anoxic phase: over aeration, over loading and the equivalence of oxygen demand and supply, are the main factors determining the blowers stopping.


Author(s):  
Regimantas Dauknys ◽  
Aušra Mažeikienė

The tertiary wastewater treatment experiment was performed on the experimental stand which was installed in a wastewater treatment plant and which consisted of three filters of the diameter of 380 mm with a non-submerged media. Biologically treated wastewater was constantly supplied to these filters. Tertiary wastewater treatment process was aggravated due to low temperature of wastewater (6 °C) and high fluctuations of load according to individual pollutants – the difference between the minimum and maximum values ranged from 3 to 10 times. The productivity of removal of pollutants according to individual contamination rates reached 8 to 43%.


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